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1 ERODIBLE DRUG DELIVERY SYSTEMS FOR TIME-CONTROLLED 1 RELEASE INTO THE GASTROINTESTINAL TRACT 2 3 Alessandra Maroni, Lucia Zema, Matteo Cerea, Anastasia Foppoli, Luca Palugan, 4 Andrea Gazzaniga* 5 6 Università degli Studi di Milano, Dipartimento di Scienze Farmaceutiche, Sezione di 7 Tecnologia e Legislazione Farmaceutiche "Maria Edvige Sangalli", Via G. Colombo 71, 8 20133 Milan, Italy. 9 *Corresponding Author: [email protected], phone +39 02 503 24654 10 11 12 *Manuscript

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Page 1: 1 ERODIBLE DRUG DELIVERY SYSTEMS FOR TIME-CONTROLLED ... A et a… · 1 1 ERODIBLE DRUG DELIVERY SYSTEMS FOR TIME-CONTROLLED 2 RELEASE INTO THE GASTROINTESTINAL TRACT 3 4 Alessandra

1

ERODIBLE DRUG DELIVERY SYSTEMS FOR TIME-CONTROLLED 1

RELEASE INTO THE GASTROINTESTINAL TRACT 2

3

Alessandra Maroni, Lucia Zema, Matteo Cerea, Anastasia Foppoli, Luca Palugan, 4

Andrea Gazzaniga* 5

6

Università degli Studi di Milano, Dipartimento di Scienze Farmaceutiche, Sezione di 7

Tecnologia e Legislazione Farmaceutiche "Maria Edvige Sangalli", Via G. Colombo 71, 8

20133 Milan, Italy. 9

*Corresponding Author: [email protected], phone +39 02 503 24654 10

11

12

*Manuscript

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Abstract 13

In oral delivery, lag phases of programmable duration that precede drug release may 14

be advantageous in a number of instances, e.g. to meet chronotherapeutic needs or 15

pursue colonic delivery. Systems that give rise to characteristic lag phases in their 16

release profiles, i.e. intended for time-controlled release, are generally composed of a 17

drug-containing core and a functional polymeric barrier. According to the nature of the 18

polymer, the latter may delay the onset of drug release by acting as a rupturable, 19

permeable or erodible boundary layer. Erodible systems are mostly based on water 20

swellable polymers, such as hydrophilic cellulose ethers, and the release of the 21

incorporated drug is deferred through the progressive hydration and erosion of the 22

polymeric barrier upon contact with aqueous fluids. The extent of delay depends on the 23

employed polymer, particularly on its viscosity grade, and on the thickness of the layer 24

applied. The manufacturing technique may also have an impact on the performance of 25

such systems. Double-compression and spray-coating have mainly been used, resulting 26

in differing technical issues and release outcomes. In this article, an update on delivery 27

systems based on erodible polymer barriers (coatings, shells) for time-controlled release 28

is presented. 29

30

Keywords 31

Oral pulsatile release, Oral colon delivery, Coating, Swellable/erodible hydrophilic 32

polymers, Injection-molding, Fused deposition modeling 3D printing. 33

34

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Introduction 35

Oral delivery systems for time-controlled release are able to defer the onset of drug 36

release into the gastrointestinal tract for a programmable lag period independent of pH, 37

ionic strength, enzyme concentration and other physiological parameters. It is by now 38

recognized that a delay prior to release may be advantageous for effective 39

pharmacological treatment of several pathologic conditions [1]. This is typically the 40

case with a variety of high-morbidity rheumatic, cardiovascular and respiratory chronic 41

diseases, which show cyclic patterns in their signs and symptoms [1,2]. When these 42

mainly recur at night or in the early morning hours, bedtime administration of drug 43

products having a proper lag phase in their release profile would help provide 44

pharmacological protection as needed. On the other hand, both untimely awakenings, as 45

an immediate-release dosage form would require, and exposure to unnecessarily 46

sustained therapeutic drug levels, as prolonged-release formulations taken before sleep 47

would entail, could thereby be overcome. As a result, not only the efficacy and safety of 48

a treatment but also the relevant patient compliance may greatly be enhanced through 49

the use of chronopharmaceutical delivery systems. 50

Besides, a lag phase prior to release allows to target the colonic region with drug 51

molecules intended for either a local action, e.g. to treat Inflammatory Bowel Disease 52

(IBD), or for systemic absorption, especially of biotech molecules that pose stability 53

issues in the proximal gut and may benefit from the aid of enhancers for mucosal 54

permeation [3,4]. When colon delivery is sought, the lag phase is expected to last 55

throughout the entire small intestinal transit (3 h ± 1 SD), which was reported not to be 56

strongly influenced by the characteristics of dosage units and by food intake [5,6]. 57

Moreover, the lag period should be started upon emptying from the stomach rather than 58

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on administration, owing to the high variability of gastric residence that cannot reliably 59

be predicted. Hence, in order to attain colonic release based on a time-controlled 60

approach, enteric coating is generally required. 61

Repeated lag phases, each followed by the release of a drug dose fraction, may be 62

exploited to fulfill multiple daily administrations regimens when prolonged release is 63

not a viable option, e.g. because of pharmacokinetic (strong first-pass effect) or 64

pharmacodynamic (tolerance) constraints. Successive release pulses are also proposed 65

as an alternative strategy in antibiotic therapy, possibly resulting in restrained growth of 66

resistant bacterial strains [7]. 67

Finally, properly modulated lag phases prior to the release of co-administered 68

bioactive compounds may avoid undesired drug-drug interactions in the gastrointestinal 69

tract and overcome the need for differing dosing schedules, thus improving the overall 70

patient convenience and compliance [8]. 71

Peroral delivery systems for time-controlled release are expected to yield lag phases 72

on the order of few hours, which may be consistent with their mean residence time 73

within the digestive tract. These are often pursued through functional polymeric barriers 74

that enclose an inner drug formulation [9,10]. According to the physico-chemical 75

properties of their polymeric components and type of excipients added (plasticizers, 76

pore formers, bulking agents), such barriers delay the onset of release via differing 77

mechanisms. They may indeed undergo time-programmed disruption, become leaky or 78

be subject to progressive erosion/dissolution. In particular, erodible systems are 79

generally single-unit dosage forms based on a drug containing-core, such as an 80

immediate-release tablet or capsule, and a swellable hydrophilic barrier of adequate 81

thickness and polymer viscosity. Such a barrier may be a coating or, in more recent and 82

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innovative instances, a freestanding release-modifying shell available for filling with 83

any drug formulation. 84

Because of the inherent safety and biocompatibility profile as well as of their 85

availability in a range of grades and reasonable costs, hydrophilic cellulose derivatives, 86

namely hydroxypropyl methylcellulose (HPMC) and, less frequently, hydroxypropyl 87

cellulose (HPC) and hydroxyethyl cellulose (HEC), are broadly used as the functional 88

polymers in erodible delivery systems [11]. Other polysaccharides, including 89

galactomannans, alginates, xanthan gum, and non-saccharide hydrophilic polymers, 90

such as polyvinyl alcohol (PVA) and polyethylene oxide (PEO), are nonetheless also 91

employed. All of these materials are largely utilized in the food, pharmaceutical, 92

nutraceutical and cosmetic industries mainly as rheology-modifiers, stabilizers, binders 93

and film-coating agents. 94

Upon water uptake, such polymers typically go through a glassy-rubbery 95

thermodynamic transition that is associated with distension and disentanglement of their 96

macromolecular chains [12-14]. Consequently, the polymer structure may expand, erode 97

due to mechanical attrition and/or dissolve at a rate that chiefly depends on the relevant 98

physico-chemical characteristics and on the ionic strength and temperature of the 99

medium. As the aqueous fluid penetrates into the polymeric layer, a swelling front, i.e. 100

the boundary between the glassy and the rubbery domain, and an erosion front, at the 101

interface between the rubbery polymer and the outer medium, are identified. Depending 102

on the relative movements of the swelling and erosion fronts, which in turn are 103

governed by the hydration, dissolution and viscosity properties of the polymer, a gel 104

layer of varying thickness is formed. 105

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In a few instances, insoluble materials are added to the hydrophilic polymers to 106

modulate the degree of hydration of the barrier, or even used as the main components of 107

mechanically erodible coatings. In the latter case, their erosion in aqueous fluids would 108

need to be promoted by surfactant excipients. 109

Drug release from hydrophilic erodible systems is in principle deferred until the 110

entire polymeric layer is in the swollen state, i.e. when the swelling front has reached 111

the drug core, possibly followed by extensive dissolution/erosion of the hydrated 112

polymer. The duration of the lag phase is indeed dictated by the physico-chemical 113

properties of the polymer employed, primarily molecular weight and degree of 114

hydrophilicity, and by the thickness of the erodible barrier. The manufacturing 115

technique, which may range from double-compression and spray-coating to hot-116

processing, can also affect the layer functionality. 117

In the following sections, oral delivery systems for time-controlled release provided 118

with an erodible polymer barrier are reviewed, and advances in this particular field are 119

illustrated with special emphasis on formulation and performance issues. 120

121

Erodible systems manufactured by double-compression 122

The manufacturing of oral delivery systems provided with erodible coatings dates 123

back to the early 90s. Until then, the use of such polymers in the manufacturing of solid 124

dosage forms was tied to tableted hydrophilic matrices for prolonged release. Indeed, 125

double-compression technique, also known as press-coating, was adopted in all initial 126

attempts. The first one concerned a three-layer tablet system that was proposed for two-127

pulse release of drugs [15,16]. Such a system was composed of two conventional drug 128

(ibuprofen) layers and a high-viscosity HPMC (Methocel® K4M and Methocel

® K15M) 129

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barrier in between. An impermeable ethylcellulose (EC) film covered the lateral area 130

and one of the bases of the assembly so that the outer surface of a single drug layer was 131

allowed to interact with solvent upon first contact with the medium. The former dose 132

fraction was thereby released, whereas the latter was released after a lag phase due to 133

the hydration and erosion of the polymer barrier. The delay between the release pulses 134

depended on the viscosity of the polymers employed, and release of the latter dose 135

fraction was slower. This was ascribed to a less efficient activation of the disintegrant 136

incorporated within the inner drug layer that was progressively exposed to the aqueous 137

fluid. The release behavior observed in vitro was reflected in two-peak plasma 138

concentration curves in healthy volunteers. However, because of its multiple-layer 139

configuration and the need for a partial coating, the system would involve serious 140

scalability issues. Therefore, a simpler press-coated formulation was designed, wherein 141

the polymer, a low-viscosity HPMC (Methocel® K100 LV), covered the entire surface 142

of the core [17]. The coated system could yield single-pulse release after a lag phase or, 143

administered in combination with an immediate-release tablet, the repeated release 144

performance attained from the previous device. In the double compression process, 145

positioning of the core tablet in the die represented a critical step. However, by correctly 146

centering it within the polymer powder bed, biconvex tablets with coatings of 147

homogeneous thickness were obtained. As desired, the in vitro release was delayed for a 148

reproducible period of time, although leaching of a small percentage of the drug content 149

prior to the quantitative release phase was inferred from the curves. This was ascribed to 150

premature outward diffusion of dissolved drug molecules through the swollen polymer 151

coating. 152

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A low- and a high-viscosity HPMC grade (Methocel® K100 and Methocel

® K4M) 153

were used, either alone or mixed with each other, as the coating agents of a delivery 154

system containing ibuprofen, aimed at the chronotherapy of rheumatoid arthritis, or 155

pseudoephedrine hydrochloride, a water-soluble model drug [18-20]. Increasing the 156

coating level or the amount of high- vs low-viscosity polymer resulted in longer lag 157

times and slower in vitro release as well as decreased absorption rates in healthy 158

volunteers. Sodium alginate, as compared with HPMC, performed as a less effective 159

barrier-forming polymer. Incorporation of a fraction of the drug dose in the coating 160

layer changed the release behavior, generally yielding biphasic kinetics that depended 161

on the composition of the polymeric coat and its drug load. 162

High-viscosity HPMC (Methocel® K4M, Methocel

® K15M and Methocel

® K100M) 163

was employed to prepare a system intended for colonic delivery of the anti-parasitic 164

drug tinidazole [21]. An enteric coating was applied externally to enable site-selective 165

release. The lag phase duration and the release rate were markedly affected by the 166

viscosity grade of the polymer, while hardness of press-coated tablets in a 40-60 N 167

range did not impact on the relevant performance. Administered to 2 healthy volunteers, 168

the system was shown to disintegrate in the ascending colon. Methocel® K100M was 169

also used to coat, at a compression force of 60-80 N, minitablet cores (3 mm in 170

diameter) intended for immediate or prolonged release of nifedipine [22]. By combining 171

differing core and coated formulations in a gelatin capsule, a variety of release patterns 172

were achieved. 173

Low-viscosity HPMC coatings were applied by an alternative tableting method 174

(One-Step Dry-Coated, OSDRC) based on the use of a specially modified equipment, 175

which was previously set up in order to overcome disadvantages typically encountered 176

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with conventional double-compression technique [23]. These mainly encompass the 177

need for poorly scalable multiple-step processing, the issue of coat thickness 178

homogeneity and difficulties in attaining relatively low coating levels. By the OSDRC 179

method, layers of 0.5-2 mm were obtained, with satisfactory thickness homogeneity and 180

practically unchanged performance within a 100-200 MPa range of compression 181

pressure. 182

High-viscosity HPMC was mixed with polyvinylpyrrolidone (PVP) at different ratios 183

and applied, by conventional double-compression technique, to minitablet cores 184

containing solid felodipine/PVP dispersions [24,25]. Mixing with PVP at 30-50% 185

resulted in improved mucoadhesion of the HPMC coating. The delays prior to a rapid 186

release of the drug increased in duration with the percentage of HPMC in the 187

formulation. In vitro delays of more than 10 h were observed with amounts of HPMC at 188

which mucoadhesive properties were enhanced. The issue of possible inconsistency 189

between duration of the lag phase and gastrointestinal transit was faced by the design of 190

a floating pulsatile delivery system aimed at gastro-retention [26]. For this purpose, a 191

verapamil hydrochloride tablet was first coated with low-viscosity HPMC (Methocel® 192

E5, Methocel® E15 or Methocel

® E50), expected to defer the onset of drug release. A 193

blend of a high-viscosity grade of the polymer (Methocel® K4M) and Carbopol

® 934P, 194

which also contained sodium bicarbonate to generate effervescence, was subsequently 195

applied to a single face of the unit coated with low-viscosity HPMC. The system was 196

proved able both to delay the onset of release and to float in vitro. Lag time depended 197

on the viscosity and amount of HPMC in the coating. A ɣ-scintigraphic evaluation in 6 198

healthy volunteers highlighted the extended gastric residence of the dosage form and 199

reproducible lag phases before release. In all cases, this occurred in the stomach or 200

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small intestine. Recently, various grades of HPMC were used to coat tablet cores based 201

on drugs with differing solubility values [27]. Poorly soluble carbamazepine was 202

released in a pulsatile fashion after erosion of the coating polymer, and the viscosity 203

characteristics of the latter strongly impacted on the relevant performance. On the other 204

hand, more soluble drugs were released in a sigmoidal mode, which was attributed to 205

their diffusion through the fully hydrated HPMC layer, and a poor influence of the 206

polymer viscosity was noticed. The outward diffusion of the drug prior to its 207

quantitative release could be prevented by inserting an enteric film below the erodible 208

coating. However, this would ultimately impart pH-dependence to the lag phase and 209

possibly hamper a timely release of the drug for chronotherapeutic purposes. The 210

amount of HPMC also affected the time and rate of release. 211

Although HPMC was most widely utilized as a coating agent intended for delaying 212

dug release, the use of other hydrophilic cellulose derivatives was reported. Particularly, 213

HPC was the component of a compressed shell that was separately prepared and, once 214

perforated, manually assembled with a cylindrical core tablet containing isosorbide-5-215

nitrate [28]. The upper and lower bases of the resulting system were coated with an 216

impermeable ethylene vinyl acetate copolymer film. Release was deferred until the 217

polymeric shell was completely eroded or detached. Lag time was affected by the 218

thickness of such a shell and by the composition of the core. Indeed, replacing 219

microcrystalline cellulose with lactose shortened the lag phase because of the osmotic 220

effect exerted by the latter filler. 221

A diltiazem hydrochloride system based on HPC was prepared by conventional 222

press-coating [29,30]. As with HPMC, the lag phase duration was modulated either by 223

increasing/decreasing the amount of coating material applied or by employing HPC, or 224

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mixtures thereof, with differing viscosity values. Prototype formulations having in vitro 225

delays of approximately 3 h and 6 h were administered to beagle dogs. A good 226

agreement was found between in vitro and in vivo data relevant to the former prototype, 227

whereas lag time in vivo was shorter than in vitro in the latter case. This gap was 228

reduced when a paddle rotation speed of 150 rpm was set instead of 100 rpm during 229

release testing. In order to assess its potential for colon delivery, the system having lag 230

time of 3 h was provided with an enteric HPMCAS film containing a gastric emptying 231

marker (phenylpropanolamine hydrochloride) [30]. The mean difference between the 232

time of first appearance in plasma (TFA) of the drug and of the marker molecule was of 233

about 3 h, which was consistent with the lag time obtained from the pH 6.8 fluid stage 234

of the in vitro test. HPC was also used in admixture with EC at a weight ratio of 7:1 235

[31]. The addition of the insoluble polymer aided a faster release of aceclofenac, 236

intended for the chronotherapy of rheumatic morning pain, after the delay period. The in 237

vitro performance of press-coated systems based on this blend was proved independent 238

of various parameters, such as the compression force, paddle rotation speed during 239

release testing and pH of the medium. Provided with an enteric-coating, the formulation 240

was administered to rabbits, showing a clear lag phase as opposed to an immediate-241

release tablet. However, due to variable residence of solid dosage forms in the stomach, 242

gastroresistance may prevent the anti-inflammatory drug from being released at the time 243

the disease symptoms occur. 244

Low-substituted HPC (L-HPC), an insoluble swellable hydrophilic cellulose ether 245

that is largely used as a disintegrant, was mixed with glyceryl behenate at differing 246

ratios and subjected to a melt-granulation process [32]. The resulting granules were 247

applied by double-compression to theophylline tablet cores to give the erodible layer. 248

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The press-coated tablet was studied in vitro and in beagle dogs, by pharmacokinetic as 249

well as ɣ-scintigraphic techniques. Lag phases were reproducible in duration and 250

increased with the amount of glyceryl behenate in the coating formula up to 75%. No 251

significant differences were found either between in vitro and in vivo lag times, or 252

between in vivo lag and disintegration times, both in the fasted and fed state. 253

Press-coated tablets for chronotherapeutic purposes were prepared from HEC 254

employed as the erodible barrier-forming material [33]. The onset of release of 255

diltiazem hydrochloride from the core was delayed in vitro as a function of the coating 256

level and the viscosity grade of HEC. The particle size of the polymer also affected lag 257

time. Using powders with larger particle dimensions was associated with shorter delay 258

phases, which was ascribed to the positive effect of a greater porosity on the polymer 259

hydration process. The role played by HEC viscosity was studied in healthy volunteers 260

[34]. When this parameter increased, progressively longer lag time (Tlag) and lower 261

maximum concentration (Cmax) values were observed in the plasma concentration vs 262

time curves. However, the area under the curve (AUC0-24 h) did not change significantly. 263

In vitro and in vivo lag times were in agreement. 264

Besides cellulose derivatives, the use of PEO as a hydrophilic erodible coating agent 265

was reported. Blended with PEG 6000 at 1:1, it was applied to tablets containing 266

acetaminophen and differing water soluble excipients, such as PEG 6000, sucrose and 267

lactose [35]. These were added in order to promote erosion of the core in the distal 268

intestine, where the press-coated tablets would be intended to release their drug load, 269

thus possibly counterbalancing the paucity of water of regional fluids. The core erosion 270

was experimentally quantified and expressed by a purposely introduced parameter, i.e. 271

the core erosion ratio. In a pharmacokinetic study conducted with fasted beagle dogs, 272

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greater Cmax and AUC values were obtained from formulations having a higher core 273

erosion ratio. The amount of PEG 600 vs PEO was raised up to 5:1 in the coating of 274

nifedipine tablets containing sucrose as an erosion enhancer [36]. In vitro lag times 275

increased with the percentage of PEO and were aligned with TFA data in beagle dogs. 276

PEO formed the swelling/erodible upper layer of a press-coated system with an 277

impermeable cellulose acetate propionate shell covering one of the bases and the lateral 278

surface [37]. The amount of polymer in the top coating affected both the time and rate 279

of release of drug molecules with different solubility. Visual monitoring of 280

morphological changes undergone by the system during in vitro testing highlighted 281

gradual expansion and erosion of the partial PEO coat until final detachment from the 282

underlying unit. Used in place of PEO, sodium alginate and sodium 283

carboxymethylcellulose had less and greater impact on the release performance, 284

respectively, consistent with their observed swelling/erosion behavior. Guar gum having 285

ten-fold higher viscosity than PEO also exerted a tighter control of the onset and rate of 286

release [38]. Increasing the core diameter or adding a soluble filler, such as lactose, to 287

PEO or guar gum top layers resulted in reduced duration of the lag phase and enhanced 288

release rate. Differing PEO grades were employed to coat tablets containing solid 289

dispersions of indomethacin in a novel sucrose fatty acid ester carrier [39]. In vitro lag 290

time depended on the viscosity and amount of the coating polymer. In 6 healthy 291

volunteers, press-coated tablet systems with in vitro lag phase of approximately 6 h 292

brought about delayed appearance of indomethacin in plasma with respect to an 293

immediate-release commercial product. However, no significant differences were found 294

in the Cmax and AUC relevant to the two formulations. 295

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Hydrophilic polymers of natural origin were also proposed as press-coating agents 296

for time-controlled delivery systems. For instance, powders composed of sodium 297

alginate and chitosan, forming a polyelectrolyte complex, and of lactose as a filler were 298

obtained by spray-drying, evaluated for flowability and compaction properties and 299

finally applied to acetaminophen tablets [40]. Through progressive erosion of the 300

coating layer, drug release was delayed in pH 6.8 fluid for a time interval that depended 301

on the chitosan content of the composite powder and on the polymer degree of 302

deacetylation. A prompt release phase was eventually observed. In pH 1.2 fluid, 303

acetaminophen was released slowly after longer delays. Prepared for comparison 304

purposes, physical mixtures of chitosan with spray-dried alginate/chitosan particles and 305

spray-dried powders composed of lactose and of pre-formed alginate/chitosan complex 306

failed to provide the desired release pattern. 307

Blends of the bacterial exopolysaccharide xanthan gum and plant galactomannan 308

locust bean gum were used in the double-compression coating of the SyncroDose™ 309

delivery system according to TIMERx® technology [41]. Differing release modes and 310

lag times were achieved by modifying the concentration and ratio of the two 311

polysaccharides, performing as synergistically interacting heterodisperse polymers. 312

313

Erodible delivery systems manufactured by spray-coating 314

The feasibility of coating techniques other than double-compression was explored for 315

the manufacturing of erodible polymer barriers able to control the onset of drug release. 316

Particularly, the goals were to establish simpler processing modes, with better industrial 317

scale-up prospects, exploit conventional production equipment and broaden the range of 318

viable core formulations (e.g. large tablets, minitablets, granules, pellets, gelatin 319

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capsules) [17]. Furthermore, some performance issues, strictly connected with the 320

structure of press-coatings, their relatively high thickness and the relevant homogeneity 321

limitations, needed to be improved. These primarily involved extended, variable and 322

poorly flexible lag times, incomplete suppression of drug leakage during the delay 323

period and impact on the subsequent release phase. Preliminary spray-coating trials 324

were thus undertaken because such a technique would have allowed continuous and 325

uniform films to be formed rather than layers of pressed powder, and fluid bed as well 326

as rotating pan equipment to be utilized instead of specially devised or modified 327

tableting machines [17,42,43]. In addition, it could in principle be adapted to substrate 328

dosage forms having diverse size, surface and density characteristics, thereby 329

circumventing the dimensional and mechanical constraints associated with double-330

compression. A limited technical background was available on the use of swellable 331

hydrophilic polymers as film-coating agents, and this mainly concerned application of 332

low-viscosity grades as thin layers with protective, taste-masking or cosmetic function. 333

Nonetheless, HPMC with marked viscosity (Methocel® K4M and Methocel

® K15M) 334

appeared potentially suitable for delaying drug release for a time interval on the order of 335

hours without binding to excessively thick coatings. The polymers were suspended in a 336

hydro-alcoholic vehicle in order to counteract the thickening effect they exert upon 337

hydration. The ratio between ethanol and water needed to be adjusted so as to enable 338

nebulization of the coating suspension at reasonable rates and polymer concentrations 339

on the one hand, and adequate coalescence of the solid particles on solvent evaporation 340

on the other. The addition of plasticizing, anti-tacking and binding excipients, such as 341

PEG 400, talc and PVP, was investigated. The coatings applied to tablets and 342

minitablets were provided with consistent thickness and smooth surface. Moreover, they 343

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yielded the desired release pattern. Considering the regulatory issues raised by organic 344

solvents, the feasibility of aqueous spray-coating by fluid bed was then evaluated using 345

HPMC having increasing viscosity, namely Methocel® E5, Methocel

® E50 and 346

Methocel® K4M [44-46]. The operating conditions, above all spray rate, inlet air 347

temperature and polymer concentration in the solutions, required an attentive set-up in 348

order to overcome major problems of powdering and nozzle clogging as well as lengthy 349

processing. The viscosity grade of the polymer chiefly affected the process time, 350

nebulization being possible only with diluted solutions that increased the spraying and 351

drying duration. From all of the polymers under investigation, coated units with 352

satisfactory physico-technological characteristics were obtained. The release behavior 353

was studied by paddle dissolution and modified disintegration apparatus. The latter 354

proved indeed better suited to prevent sticking of swollen HPMC to the vessels, thus 355

providing more reliable data. By both testing methods, a prompt release after a lag 356

phase was highlighted, which depended on the coating level and the polymer viscosity. 357

Using Methocel® E50 resulted in acceptable process feasibility, ability to delay drug 358

release and fine-tuning of the lag phase. Moreover, the coating process was shown 359

robust and potentially scalable. In the case of Methocel® K4M, not only the coating 360

operations were strongly impaired by the high viscosity of water solutions, but also a 361

small amount of drug was slowly released from coated units toward the end of the delay 362

period. This was attributed to the formation of a firm, poorly erodible gel structure 363

ultimately rupturing with the aid of the inner tablet disintegration upon water influx 364

[47]. When the Methocel® E50-based coating procedure was applied to hard- and soft-365

gelatin capsules instead of tablets, the process parameters needed to be adjusted in order 366

to prevent the sticking and shrinking of the shells [48]. In order to streamline 367

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manufacturing of Methocel® E50-coated systems, alternative techniques, such as 368

tangential-spray film-coating and powder-layering carried out by fluid bed 369

rotogranulator, were attempted. Preliminary studies in volunteers demonstrated that, 370

irrespective of the core dosage form, delivery systems coated with Methocel® E50 by 371

aqueous spray-coating were able to defer drug appearance in saliva as a function of the 372

coating level [45,48]. The in vitro and in vivo lag phases were comparable in duration. 373

Moreover, when provided with a gastroresistant film, labeled formulations were shown 374

to consistently break up in the ascending colon. After low-molecular weight drugs, 375

chosen as models because of their stability characteristics and easy analysis, the 376

possibility of conveying bovine insulin by this delivery system was explored [48-52]. In 377

order to increase the chances of preserving integrity of the protein and promoting its 378

permeation through the intestinal mucosa, enzyme inhibitor and absorption enhancer 379

adjuvant compounds were incorporated in the formulation. Insulin was proved to 380

withstand all manufacturing steps, as inferred by assaying the degradation products 381

mentioned by European Pharmacopoeia, and was released in vitro in a pulsatile mode, 382

as previously observed with antipyrine and acetaminophen, along with the adjuvants. 383

The latter were also applied as a separate film enclosed between two Methocel® E50 384

layers, so that their release would occur earlier than that of the protein drug contained in 385

the core, and less threatening conditions could be established in vivo beforehand 386

[53,54]. 387

When erodible coatings were applied to minitablet cores, relatively larger amounts of 388

polymer were found necessary than with single units in order to obtain lag times 389

potentially suitable for chronotherapeutic or colonic release purposes [55-57]. Thus, the 390

thickness of the resulting film coatings would ultimately fail to comply with the size 391

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requirements of multiple-unit dosage forms. Besides, depending on the viscosity grade 392

of the polymer employed, the rate of release at the end of the lag phase would most 393

likely be reduced. With the aim of overcoming this formulation issue, the external 394

application of an insoluble, flexible and increasingly leaky film was proposed. Such a 395

film was mainly intended to slow the uptake of water by the underlying HPMC layer, 396

and consequently the relevant hydration as well erosion processes, without acting as a 397

major mechanical constraint to the polymer expansion. Eudragit® NE 30 D was selected 398

as the film-forming agent, whereas various superdisintegrants, above all Explotab® V17, 399

were added as especially effective non-conventional pore formers. After tuning the 400

composition of the outer film and the ration between HPMC and polymethacrylate 401

coating levels, the desired release performance and dimensional characteristics were 402

obtained from formulations based on this novel two-layer design. 403

HPMC barriers derived from coalescence of polymer particles were prepared not 404

only by spray-coating but also by dipping, which circumvented the technical difficulties 405

associated with nebulization of highly viscous polymeric solutions [58]. Ethanol/water 406

mixtures were used to disperse the HPMC powder. Immersion steps, each followed by 407

manual hot-air drying, were repeated until the tablets had reached the established weight 408

gain. The latter was related to the lag phase duration. By affecting the structure of the 409

coat layer, parameters such as the ethanol/water volume ratio, the concentration of the 410

polymer and the time during which it was allowed to swell in the hydro-organic vehicle 411

also impacted on the release of nifedipine from the core tablet. 412

Waxy materials of natural origin, in admixture with a surfactant, were employed as 413

an alternative to swellable hydrophilic polymers in order to attain erodible barriers for 414

time-controlled release [59]. Spraying of water dispersions of such lipophilic coating 415

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agents required that the processing temperature be set at relatively high values (75°C). 416

The resulting delivery system (Time Clock

) proved suitable for deferring salbutamol 417

sulfate release in vitro and in healthy volunteers. In both cases, the lag phases were 418

clearly dependent on the coating level. An agreement between in vitro and in vivo data 419

was achieved when media having increased viscosity were used for release testing, 420

which led to longer in vitro delays. The performance of the system in the 421

gastrointestinal tract was demonstrated not to be influenced by food intake in 6 subjects, 422

and AUC0-∞ as well as Cmax in the fasted state were consistent with those of an 423

immediate-release reference product. The Time Clock

system provided time-based 424

colonic delivery in humans when in gastro-resistant configuration, as highlighted by ɣ-425

scintigraphy [60]. This was confirmed in 8 fed volunteers through pharmaco-426

scintigraphic evaluation of a 5-aminosalicylic acid-containing formulation [61]. 427

428

Erodible delivery systems manufactured by hot-processing techniques 429

Hot-processing techniques, which enable the production of high-density structures of 430

any desired form from softened/melted thermoplastic material substrates, are raising 431

huge interest in every manufacturing area. However, their exploitation in the 432

pharmaceutical field is still fairly limited despite the enormous potential held [62-65]. It 433

is only recently that drug delivery applications mainly of hot-melt extrusion (HME), 434

injection-molding (IM) and three-dimensional (3D) printing by fused deposition 435

modeling (FDM) have been investigated and reported. Interestingly, the use of such 436

techniques was proposed for the production of void functional capsule shells 437

independent of their core units, with considerable prospective advantages from both the 438

technical and the regulatory point of views [66-68]. In this respect, the feasibility of IM 439

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in fabrication of erodible shells intended to defer release of their contents was explored 440

[66]. HPC of various viscosity grades was selected as the capsule-forming polymer 441

because of the inherent thermoplastic behavior upon heating. A bench-top IM press was 442

employed, and the design of a specially suited mold was required. Through its use, cap 443

and body items were obtained within single automated production cycles. In vitro 444

studies pointed out a rapid release of the model drug after lag times that, composition 445

being equal, correlated with the thickness of shells in the 300-900 µm range 446

investigated. By visual inspection of capsule systems immersed in deionized water, it 447

was inferred that release after the delay phase would be connected with rupturing of the 448

hemispherical top and bottom ends of the device that were thinner than the cylindrical 449

region where cap/body portions overlapped. On administration of these prototypes to 3 450

healthy volunteers, the in vivo lag times calculated from salivary concentration curves 451

of acetaminophen were found in linear relationship with the in vitro ones [69]. The 452

design of a novel mold for 600 µm thick units and concomitant setting up of proper 453

formulation as well as operating parameters were subsequently undertaken [70]. This 454

allowed faster production cycles to be carried out without adding external or internal 455

lubricants. The shells obtained showed improved mechanical properties, which would 456

aid large-scale filling by the equipment used with conventional gelatin capsules, and 457

less variable thickness that was also closer to the theoretical value. Besides, the issue of 458

thicker body/cap overlap areas was overcome. As a result, more reproducible release 459

profiles were attained. The time to shell opening was demonstrated consistent 460

irrespective of differing types of solid dosage forms conveyed (fine powder, granules, 461

pellets, solid dispersion). These HPC capsules were successfully subjected to enteric 462

coating, with no need for sealing the assembled caps and bodies, and then to final curing 463

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[71]. Such systems fulfilled the requirement of resistance in pH 1.2 medium for 2 h, 464

while maintaining the original pulsatile release curves when tested in pH 6.8 phosphate 465

buffer. Accordingly, they appeared potentially suitable for time-dependent colon 466

delivery, provided that the shell thickness be properly modulated so that duration of the 467

in vivo lag phase would match the small intestinal transit time. 468

Capsule shells composed of HPC were lately replicated by FDM 3D printing, starting 469

from filaments purposely prepared in-house by HME [68]. After assessing the 470

possibility of attaining hollow structures by the use of FDM and developing the needed 471

computer-aided design (CAD) files, bodies and caps of the shells were manufactured. 472

Overall, these exhibited satisfactory physico-technological characteristics and, 473

assembled into a drug-containing device, the typical lag phase before a rapid and 474

quantitative release. Upon contact with deionized water, the behavior of capsule shells 475

fabricated by FDM was comparable with that of analogous molded systems, thus 476

supporting the real-time prototyping potential of this 3D printing technique and its 477

possible exploitation in formulation development studies aimed at IM production. 478

Based on the expertise gained from the manufacturing of functional capsule shells, 479

cylindrical dosage forms, such as immediate- and prolonged-release polymeric units, 480

were also fabricated by HME and IM [72,73]. The relevant production via hot-481

processing was found to offer inherent advantages over the established techniques. 482

483

Conclusions 484

Drug delivery systems able to incorporate a lag phase of pre-established duration in 485

their release patterns are a topic of high current interest, primarily in connection with 486

oral chronotherapy and colon targeting. 487

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Among the numerous formulation strategies proposed, those based on erodible 488

polymeric barriers have largely and successfully been exploited. As the main 489

components of such barriers, swellable/erodible polymers of hydrophilic nature, such as 490

HPMC and other cellulose derivatives, have especially been used. Indeed, they easily 491

enable fine-tuning of the release performance in terms of time and also rate through 492

proper selection of the type and amount of polymer, which will affect the thickness and 493

viscosity of the layer upon hydration. Erodible barriers intended for time-controlled 494

release generally consist in coating layers. These may partially or entirely enclose a 495

drug-containing core thus preventing it from immediately being exposed to aqueous 496

fluids on administration of the dosage form. Coatings may be applied by differing 497

techniques and, accordingly, possess diverse structural and functional characteristics. 498

Apart from coating layers, which are necessarily associated with a specific core 499

formulation, polymeric barriers in the form of erodible shells have recently been 500

manufactured by hot-processing, namely via IM and FDM. Because of the great 501

versatility in terms of design, high innovative content, excellent scale-up prospects and 502

unique benefits related to a separate development as well as production, these capsule 503

shells may open up new ways in the field of time-controlled release and, more broadly, 504

in the oral delivery area. 505

506

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